Chemical Properties of Ethane, iodo- (CAS 75-03-6)

InChI

InChI=1S/C2H5I/c1-2-3/h2H2,1H3

InChI Key

HVTICUPFWKNHNG-UHFFFAOYSA-N

Formula

C2H5I

SMILES

CCI

Molecular Weight¹

155.97

CAS

75-03-6

Other Names

• 1-Iodoethane
• C2H5I
• ETHYL IODIDE
• Ethyljodid
• HYDRIODIC ETHER
• Iodoethane
• Jodethan
• Monoiodoethane
• NSC 8825

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.1840		KDB
PAff	724.80	kJ/mol	NIST
BasG	698.30	kJ/mol	NIST
ΔcH°liquid	[-1466.00; -1462.50]	kJ/mol
ΔcH°liquid	-1462.50 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-1466.00 ± 2.00	kJ/mol	NIST
μ	1.70	debye	KDB
ΔfG°	21.35	kJ/mol	KDB
Rg	0.2775		KDB
ΔfH°gas	[-8.80; -5.40]	kJ/mol
ΔfH°gas	-8.37	kJ/mol	KDB
ΔfH°gas	-7.20 ± 0.80	kJ/mol	NIST
ΔfH°gas	-8.40	kJ/mol	NIST
ΔfH°gas	-8.80 ± 0.80	kJ/mol	NIST
ΔfH°gas	-5.40	kJ/mol	NIST
ΔfH°liquid	[-39.50; -35.00]	kJ/mol
ΔfH°liquid	-39.10 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-39.50 ± 1.70	kJ/mol	NIST
ΔfH°liquid	-35.00	kJ/mol	NIST
ΔfusH°	5.34	kJ/mol	Joback Calculated Property
ΔvapH°	[29.80; 32.05]	kJ/mol
ΔvapH°	32.05	kJ/mol	NIST
ΔvapH°	31.70	kJ/mol	NIST
ΔvapH°	31.90 ± 0.10	kJ/mol	NIST
ΔvapH°	31.93 ± 0.02	kJ/mol	NIST
ΔvapH°	29.80 ± 0.30	kJ/mol	NIST
IE	[9.30; 9.60]	eV
IE	9.35 ± 0.00	eV	NIST
IE	9.35 ± 0.00	eV	NIST
IE	9.33	eV	NIST
IE	9.33	eV	NIST
IE	9.30	eV	NIST
IE	9.35	eV	NIST
IE	9.35 ± 0.01	eV	NIST
IE	9.35 ± 0.02	eV	NIST
IE	9.35	eV	NIST
IE	9.35	eV	NIST
IE	9.37	eV	NIST
IE	9.37	eV	NIST
IE	9.35 ± 0.02	eV	NIST
IE	9.33 ± 0.01	eV	NIST
IE	9.35 ± 0.01	eV	NIST
IE	9.35	eV	NIST
IE	9.33	eV	NIST
IE	9.34	eV	NIST
IE	Outlier 9.60	eV	NIST
IE	9.45 ± 0.02	eV	NIST
IE	9.34	eV	NIST
log10WS	[-1.60; -1.60]
log10WS	-1.60		Aq. Solubility Prediction
log10WS	-1.60		Estimated Solubility
logPoct/wat	1.441		Crippen Calculated Property
McVol	64.860	ml/mol	McGowan Calculated Property
Pc	4700.00	kPa	KDB
Inp	[586.00; 621.00]
Inp	614.00		NIST
Inp	621.00		NIST
Inp	607.00		NIST
Inp	586.00		NIST
Inp	617.60		NIST
Inp	591.00		NIST
Inp	598.00		NIST
Inp	609.00		NIST
Inp	602.00		NIST
Inp	616.00		NIST
Inp	602.00		NIST
Inp	601.00		NIST
Inp	600.00		NIST
Inp	601.00		NIST
Inp	614.00		NIST
Inp	591.00		NIST
Inp	601.00		NIST
Inp	602.00		NIST
I	[876.00; 901.65]
I	901.65		NIST
I	899.84		NIST
I	896.49		NIST
I	892.00		NIST
I	881.00		NIST
I	876.00		NIST
I	892.00		NIST
I	880.00		NIST
I	881.00		NIST
I	901.65		NIST
Tboil	[344.20; 346.35]	K
Tboil	345.60	K	KDB
Tboil	345.50	K	Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
Tboil	Outlier 344.20	K	NIST
Tboil	345.50	K	NIST
Tboil	345.60	K	NIST
Tboil	345.57 ± 0.10	K	NIST
Tboil	345.45 ± 0.40	K	NIST
Tboil	346.35 ± 0.30	K	NIST
Tboil	345.45 ± 0.25	K	NIST
Tboil	345.50 ± 0.50	K	NIST
Tboil	345.52 ± 0.25	K	NIST
Tboil	345.85 ± 0.30	K	NIST
Tboil	345.50 ± 0.40	K	NIST
Tboil	345.40 ± 1.00	K	NIST
Tc	554.00	K	KDB
Tfus	[162.05; 165.00]	K
Tfus	165.00	K	KDB
Tfus	163.62	K	Aq. Solubility Prediction
Tfus	162.05 ± 0.40	K	NIST
Tfus	162.30 ± 0.40	K	NIST
Vc	0.236	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[74.51; 98.71]	J/mol×K	[338.30; 544.92]
Cp,gas	74.51	J/mol×K	338.30	Joback Calculated Property
Cp,gas	79.14	J/mol×K	372.74	Joback Calculated Property
Cp,gas	83.52	J/mol×K	407.17	Joback Calculated Property
Cp,gas	87.65	J/mol×K	441.61	Joback Calculated Property
Cp,gas	91.55	J/mol×K	476.05	Joback Calculated Property
Cp,gas	95.23	J/mol×K	510.48	Joback Calculated Property
Cp,gas	98.71	J/mol×K	544.92	Joback Calculated Property
Cp,liquid	[109.70; 115.10]	J/mol×K	[298.00; 298.15]
Cp,liquid	115.10	J/mol×K	298.00	NIST
Cp,liquid	109.70	J/mol×K	298.15	NIST
η	[0.0004224; 0.0050904]	Pa×s	[170.36; 338.30]
η	0.0050904	Pa×s	170.36	Joback Calculated Property
η	0.0025088	Pa×s	198.35	Joback Calculated Property
η	0.0014730	Pa×s	226.34	Joback Calculated Property
η	0.0009723	Pa×s	254.33	Joback Calculated Property
η	0.0006970	Pa×s	282.32	Joback Calculated Property
η	0.0005305	Pa×s	310.31	Joback Calculated Property
η	0.0004224	Pa×s	338.30	Joback Calculated Property
ΔvapH	[29.44; 34.70]	kJ/mol	[273.50; 345.60]
ΔvapH	32.00	kJ/mol	273.50	NIST
ΔvapH	34.70	kJ/mol	282.00	NIST
ΔvapH	33.60	kJ/mol	309.00	NIST
ΔvapH	31.70	kJ/mol	318.00	NIST
ΔvapH	29.77	kJ/mol	345.60	KDB
ΔvapH	29.44	kJ/mol	345.60	NIST
Pvap	101.30	kPa	345.50	Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
n0	1.50950		298.15	Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
ρl	[1923.80; 1950.00]	kg/m3	[293.00; 298.15]
ρl	1950.00	kg/m3	293.00	KDB
ρl	1923.80	kg/m3	298.15	Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
γ	0.03	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[251.46; 368.73]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45544e+01
Coefficient B			-3.07804e+03
Coefficient C			-3.57160e+01
Temperature range, min.			251.46
Temperature range, max.			368.73
Pvap	1.33	kPa	251.46	Calculated Property
Pvap	3.00	kPa	264.49	Calculated Property
Pvap	6.20	kPa	277.52	Calculated Property
Pvap	11.89	kPa	290.55	Calculated Property
Pvap	21.40	kPa	303.58	Calculated Property
Pvap	36.47	kPa	316.61	Calculated Property
Pvap	59.27	kPa	329.64	Calculated Property
Pvap	92.45	kPa	342.67	Calculated Property
Pvap	139.08	kPa	355.70	Calculated Property
Pvap	202.64	kPa	368.73	Calculated Property
Pvap	[1.10e-04; 5970.39]	kPa	[162.05; 561.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.81996e+01
Coefficient B			-5.85116e+03
Coefficient C			-8.13893e+00
Coefficient D			7.75920e-06
Temperature range, min.			162.05
Temperature range, max.			561.00
Pvap	1.10e-04	kPa	162.05	Calculated Property
Pvap	0.04	kPa	206.38	Calculated Property
Pvap	1.47	kPa	250.71	Calculated Property
Pvap	15.74	kPa	295.03	Calculated Property
Pvap	83.55	kPa	339.36	Calculated Property
Pvap	289.13	kPa	383.69	Calculated Property
Pvap	761.73	kPa	428.02	Calculated Property
Pvap	1679.28	kPa	472.34	Calculated Property
Pvap	3291.20	kPa	516.67	Calculated Property
Pvap	5970.39	kPa	561.00	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, iodo-.

Mixtures

• Toluene + Ethane, iodo-
• Ethane, iodo- + Methyl Alcohol
• Ethane, iodo- + Ethanol
• 1-Propanol + Ethane, iodo-
• Toluene + Ethane, iodo- + Methyl Alcohol
• Toluene + Ethane, iodo- + Ethanol
• 1-Propanol + Toluene + Ethane, iodo-
• Ethane, iodo- + Propanoic acid
• Propanoic acid, ethyl ester + Ethane, iodo-
• Ethane, iodo- + Methyl Alcohol + Water
• Ethane, iodo- + Ethanol + Water
• 1-Propanol + Ethane, iodo- + Water

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
• Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.